Photocatalytic removal of 2-chlorophenol from water by using waste eggshell-derived calcium ferrite

A new approach to recycling low-value eggshell food waste was to produce a CaFe2O4 semiconductor with a narrow band gap (Eg = 2.81 eV) via hydrothermal treatments of powdered eggshell suspended in aqueous ferric salt (Fe3+) solutions at varying Fe loadings. It was possible to obtain a single phase of CaFe2O4 without any Ca(OH)2 and CaO impurities using an optimal Fe loading (30 wt% of Fe3+ by eggshell weight). The CaFe2O4 material was used as a photocatalyst for the breakdown of 2-chlorophenol (2-CP, a herbicide model chemical) as a pollutant in water. The CaFe2O4 with a Fe loading of 7.1 wt% exhibited a high 2-CP removal efficiency of 86.1% after 180 min of UV-visible light irradiation. Additionally, the eggshell-derived CaFe2O4 photocatalyst can be effectively reused, giving a high removal efficiency of 70.5% after the third cycle, without the requirement of regeneration processes (washing or re-calcination). Although radical trapping experiments confirmed that hydroxyl radicals were generated in the photocatalytic reactions, photogenerated holes play a significant role in the high 2-CP degradation efficiencies. The performance of the bioderived CaFe2O4 photocatalysts in the removal of pesticides from water demonstrated the benefits of resource recycling in the area of materials science and in environmental remediation and protection.


Introduction
Chlorophenol is one of the most persistent herbicides, and according to the Environment Protection Agency (EPA), 2chlorophenol (2-CP) is one of the environmental priority pollutants due to its high toxicity and poor biodegradation. This is a result of the high stability of the C-Cl bond in the 2-CP structure. [1][2][3] As industrialized farming needs to ensure high yields of excellent quality, i.e., good-looking fruits or vegetables free from insect damage, many farmers apply a large amount of pesticides in their farmlands. Typically, the run-off containing residual pesticides results in water pollution and the pesticides enter the food-chain of aquatic plants and animals. Adsorption is one promising method for the removal of chlorophenol in contaminated water. However, the adsorption method required a relatively high adsorbent dosage (1 g L −1 to 25 g L −1 ) and further processes to degrade such pollutants. [4][5][6] Alternatively, photocatalysis technology has received considerable attention owing to its outstanding performance in the degradation of a wide range of toxic and non-degradable pollutants in water, converting them to less-toxic molecules and/or carbon dioxide. The photocatalytic wastewater treatments produce no sludge waste, hence being potentially cost effective. 7-10 Photocatalytic ozonation was reported as a superior effective method to ozonation and Fenton oxidation in the removal of dichlorophenol in a dielectric barrier discharge under varying gas atmospheres. 11,12 Ozone is added into the reactor as an oxidant to enhance the dichlorophenol degradation processes. In many reports, several synthesized photocatalysts, e.g., chemically modied TiO 2 , CuInS 2 /TiO 2 and TiO 2 /AgInS 2 heterojunctions, were applied in the degradation of chlorophenols without the requirement of any oxidant addition. [13][14][15][16] However, the reported photocatalysts have some drawbacks, requiring expensive and high-purity precursors in multi-step preparation processes.
As a semiconductor, calcium ferrite (CaFe 2 O 4 ) has been extensively applied as a photoactive material for many applications, such as CO 2 conversion, 17 solar water oxidation, 18 hydrogen production, 19,20 ferrite pigments 21 and photocatalyst for water depollution. 22 The co-precipitation method is a simple and cost-effective route to produce calcium ferrites, while calcium and ferric (ferrous) salts are commonly utilized as precursors. [22][23][24] Since mining for nite resources may become more expensive and impractical in the future, wastes or renewable raw materials have also gained popularity due to their sustainable nature and potential to reduce carbon emissions. It has been reported that a spinel calcium ferrite can be prepared from steel industry waste and from the recycling of electric arc furnace dust. 25 This innovative approach not only reduces waste, but also creates value of such waste in the area of photocatalyst development.
Eggshells, a biobased calcium source, are potentially renewable feedstocks for the materials development industry, serving as an alternative to high-purity chemicals or nite limestone. Eggshell food waste, containing CaCO 3 as the main composition, can be sorted, recovered and utilized in industries, such as fertilizer, animal feed, cement tile, sorbents, and biodiesel production plants. 26 One of the reports given by the WATT Global Media's Executive Guide to World Poultry Trends suggested a large quantity of eggshell waste, around 8.58 million metric tons of worldwide, in 2018. 26 Calcinations of eggshell produced CaO, which is a common raw material in glass, cement, paper, and high-grade steel plants. To use bioresources (or wastes) in material synthesis, it is important to determine the optimum process to produce a high-value material with high purity. This report aims to propose a green synthesis approach using waste eggshells (abundant, low-value, and renewable resources) as a calcium precursor in CaFe 2 O 4 production. In addition, the photocatalytic performance of CaFe 2 O 4 materials in the treatment of aqueous 2-cholophenol (a biocide and antiseptic substance) was investigated, exploring the photocatalytic activity, including the determination of key factors inuencing the photocatalytic activity of bio-waste derived materials. This work should broaden insight into the relationships among the composition, physiochemical (including optical) properties, and the photocatalytic activity of the materials. The results and key ndings from this research may also promote sustainable food waste utilization via creating an additional application of eggshell waste as a raw material in the production of high-value semiconducting materials being used in various applications not only for the remediation of agricultural wastewater, but also photoactive, magnetic and drug delivery applications. 27,28 Additionally, the use of renewable raw materials can contribute to the development of a circular economy by reducing waste and promoting resource efficiency.

Photocatalyst preparation
Calcium ferrite, a QES-based photocatalyst, was prepared by using the modied method reported by our group. 29 Firstly, dried powdered QES was sieved (400 mesh) to obtain particles with the particle sizes lower than 37 mm. Calcination of QES at 750°C for 6 h resulted in CaO. Secondly, FeCl 3 (3 g) dissolved in DI water (200 mL) was mixed with QES (7 g). Next, the suspension was sonicated for 30 min. Thereaer, the mixture was transferred to a Teon-lined stainless steel reactor for hydrothermal treatment (120°C, 4 h), followed by calcination at 750°C for 6 h. It should be noted that 10Fe/QES and 20Fe/QES were prepared with similar preparation procedures, varying the Fe loadings (10-20 wt% with respect to that of QES). The calcinations resulted in ca. 50% mass loss of the uncalcined samples due to the conversion of CaCO 3 to CO 2 .

Photocatalyst characterizations
Phase identication of the powdered samples was performed by Powder X-ray Diffraction (PXRD) technique on a Bruker AXS model D8 Advance diffractometer equipped with Cu Ka radiation (l = 1.5418 Å), 40 mA and 40 kV, 2q range = 5-80°, step = 0.075°, scan step = 0.2°s −1 . The crystalline phases of all samples were identied based on reference data from the Joint Committee on Powder Diffraction Standards (JCPDS) database. Microstructural studies of the catalysts were performed on a scanning electron microscope (SEM; Hitachi: SU8010). The samples were coated with platinum prior to study by SEM. The surface chemical composition/species of the samples was studied using X-ray photoelectron spectroscopy (XPS; Kratos Model Axis ultra DLD). The samples are excited with X-ray hybrid mode 700 × 300 mm spot area with a monochromatic Al Ka 1,2 radiation at 1.4 keV. All spectra are calibrated using the C 1s line (binding energy; BE = 285.0 eV). The optical band gap energy of the prepared samples was observed by UV-vis diffuse reectance spectroscopy (DRS, Shimadzu, UV-2600) with BaSO 4 as a reference. FTIR-ATR spectra were measured on a spectrophotometer (Thermo Scientic, Nicolet 6700) within the range of 4000 to 400 cm −1 , using 16 scans of accumulations at 4 cm −1 of resolution. X-ray uorescence spectroscopy (XRF, Horiba, XGT-9000) was employed to measure the bulk concentration of elements in the samples. ESR spectra were measured at 25°C, using a power of 20.02 mW and a frequency of 9.84 GHz on a Bruker Elexys E500 cw X-band ESR spectrometer equipped with an Oxford ITC605 temperature controller.

Photocatalytic activity screening test and reusability
In the photocatalytic degradation batch testing, the as-prepared photocatalyst powder (2.5 g L −1 ) was rstly suspended under magnetic stirring in synthetic wastewater containing 2-chlorophenol (2-CP, 25 ppm, 10 mL) in the dark for 30 min to reach adsorption-desorption equilibrium. When xFe/QES (x = % Fe loading) was added to 2-CP (aq), the pH of the solution increased from 6.0 to 12. Then, each suspension was illuminated (UV-vis radiation, OSRAM Ultra-vitalux 300 W × 2; l > 280 nm) at different reaction times (30,60,120, and 180 min), at a temperature of 35.0 ± 3.0°C. 30 A syringe lter (0.45 mm nylon lter membrane) was used to withdraw the treated 2-CP(aq) from each batch reactor for UV-vis absorption spectrum measurement (GENESYS 10s UV-Vis spectrophotometer). The concentration of 2-CP was monitored by measuring the absorbance at l = 237 nm, 31-33 following the protocol reported previously. [34][35][36] The % photocatalytic degradation efficiencies were calculated using the formula below.
where C 0 is the initial concentration of the pollutant model (25 ppm) and C t is the concentration of the pollutant model aer treatment aer specic treatment times. To conrm the 2-CP degradation, the total organic carbon (TOC) values were measured for the treated 2-CP(aq). The TOC values of the treated 2-CP (aq) solutions were determined on a TOC analyzer (analyticjena, Multi N/C 2100 S). Then, the TOC removal efficiencies were calculated as follows.
where TOC 0 is the initial TOC value of the 25 ppm 2-CP (aq), and TOC t is the TOC content aer treatment at particular treatment periods.
Furthermore, reusability tests were carried out while the treated 2-CP (aq) was decanted aer centrifugation, and fresh 25 ppm 2-CP (aq) was added in the batch reactor to examine the photocatalytic activity of the spent catalyst in subsequent runs (180 min treatments). Notably, the spent photocatalyst was reused in the next run without washing or any regeneration.

Degradation product determination
Gas chromatography-mass spectrometry (GC-MS, Agilent Technologies 5977B MSD) was employed to identify any 2-CP degradation products in the treated aqueous 2-CP, using the previously reported protocol with small adjustment. 3,37 The GC-MS measurements were performed by using a DB-5MS column, having dimensions of 30 m × 0.25 mm × 0.25 mm with the injection volume of the sample at 1 mL (ow 1.0 mL min −1 ). The controlled oven temperature program included maintaining at 60°C for 1 min, and increasing by 20°C min −1 up to 300°C.

Probing of reactive oxygen radicals (OHc and O 2 c − ) and holes (h + )
Semi-quantitative analysis of reactive oxygen species (such as OHc and O 2 c − radicals) and photogenerated holes in the studied photocatalysis system was carried out by electron spin resonance (ESR) techniques using aqueous 5,5,-dimethylpyrroline N-oxide (DMPO, TCI chemical purity >97%) spin trapping. [38][39][40] The as-prepared catalyst (10 mg) was suspended in a 2-CP aqueous solution (25 ppm, 4 mL) under magnetic stirring for 30 min in the dark. Subsequently, aqueous DMPO (50 mmol L −1 , 1 mL) was added in the suspension for 2 min well mixing, followed by ltering using a 0.45 mM syringe lter. The ESR spectrum of the ltered sample was measured using the same protocol as that of the aqueous 2-CP solution aer adsorption treatments. On the other hand, the suspensions of catalyst sample in DMPO/2-CP (aq) that underwent adsorption treatment were subjected to UV-vis light irradiation (OSRAM Ultravitalux 300 W × 2; l > 280 nm as a light source) at given time intervals (15, 30 and 60 min), followed by ESR measurements. In the case of O 2 c − probing, an identical procedure was carried out. However, methanolic DMPO was used to enhance the ESR signals. For comparison, QES-750 and Fe loaded QES-750 underwent similar tests to conrm whether any reactive oxygen species were generated by the ferrite precursor materials.

Scavenger tests
The scavenging test was carried out following the protocol previously reported. 41,42 Three scavenging agents, ammonium oxalate (AO), benzoquinone (BQ) and isopropyl alcohol (IPA), were each added into 2-CP (aq) at the 2-CP-to-scavenger molar ratio of 1 : 2, to quantify the amount of photogenerated holes, O 2 c − and OHc radicals, respectively. Despite being a reducible organic compound, BQ is sufficiently effective to trap holes, and suppressed the 2-CP degradation rate at pH 12. The intensity of the absorption peak at l = 237 nm does not overlap with any other peaks that correspond to other degradation products and BQ. The lower 2-CP removal efficiencies obtained in the scavenging agent-containing systems reected the effective scavenging reactions. 41,42 Results and discussion

Materials characterization
Powder X-ray diffraction (PXRD) patterns for the Fe-loaded quail eggshell (10-30% wt Fe/QES) aer calcination are shown in Fig. 1. Notably, uncalcined eggshell was denoted as QES (or uncalcined QES), whereas the calcined eggshell was denoted as QES-750. The calcined Fe-loaded eggshell is denoted as xFe/ QES, while x = % FeCl 3 loading with respect to the eggshell weight. It was observed that uncalcined QES mainly consisted of crystalline calcium carbonate (CaCO 3 ), showing a major peak at 2q = 29.5°. 43 Aer calcination at 750°C, decomposition of CaCO 3 in the QES resulted in the formation of CaO and Ca(OH) 2 (or hydrated CaO), resulting from CaCO 3 decomposition, in excellent agreement with previous studies. 43,44 With Fe loading, the 10Fe/QES and 20Fe/QES samples contained a mixture of Ca(OH) 2 , CaO and CaFe 2 O 4 . 45 Based on the diffraction proles, only the 30Fe/QES sample comprises CaFe 2 O 4 , along with unreacted CaCO 3 as the minor phase (2q = 29.5°). Hence, 30% FeCl 3 loading is the optimum condition in the preparation of the highest purity of CaFe 2 O 4 . The amount of CaO phase (if present) in the 30Fe/QES sample is lower than the detection limit of powder diffraction techniques.
Surface chemical compositions of the prepared samples were determined by XPS, and the results are shown in Fig. 2. The C 1s spectrum (Fig. 2a) of all samples shows two main peaks at 285.0 and 289.5 eV, corresponding to C-C of the surface contaminated adventitious carbon and O-C]O of the carbonate compound. 46 The QES-750 showed a highly intense peak corresponding to the carbonate functional group (at 289.5 eV). In addition, all samples exhibited two peaks in the Ca 2p region (Fig. 2b), attributed to Ca 2p 3/2 (347.0 eV) and Ca 2p 1/2 (350.5 eV). In addition, O 1s (Fig. 3c) was detected in all samples at the binding energy of 531.0 eV. In Fig. 2d, all Fe loaded samples showed two deconvolution peaks at binding energies of 712. 4 eV and 726.2 eV, which corresponded to the Fe 2p 3/2 and Fe 2p 1/2 of CaFe 2 O 4 . 47,48 It should be noted that the peak    intensity of Fe 2p increased with increased Fe content (10 to 30 wt%), accounting for 1.8 wt% (10Fe/QES), 4.0 wt% (20Fe/ QES) and 7.1 wt% (30Fe/QES). XPS is a surface technique (∼10 nm deep from the outer surface), 49,50 and the concentration of Fe at the surface may be different from that in bulk. The catalytically active sites at the surface are important to the bulk for surface reactions, including the 2-CP degradation in this work. The high bulk concentration of Fe in 30Fe/QES is found to be 36%, which is more than the theoretical value, possibly because XRF is not suitable for the concentration determination of light elements (i.e., carbon from CaCO 3 ). The catalytically active sites at the surface are important for surface reactions. Notably, the XPS peaks agree well with the PXRD data, suggesting the presence of CaO, CaCO 3 and CaFe 2 O 4 in the 10Fe/ QES and 20Fe/QES samples.
UV-vis diffuse reectance spectroscopy (UV-DRS) was employed to investigate the light-responsive characteristics of the studied materials. In comparison with QES-750, the absorption edges of the calcined Fe-modied QES samples were found to be slightly shied to longer wavelengths, along with a new broad absorption peak at ∼450-600 nm (Fig. 3a). Thus, the absorption spectra of the Fe-loaded QES materials indicated that they tend to be responsive to visible light. Additionally, the optical band gap energy (E g ) was evaluated by extrapolating the linear portion of the curve plotted from the Tauc function versus light energy 51-53 shown in Fig. 3b, exhibiting E g values of 3.71, 3.24, 3.18, and 2.81 eV for the QES-750, 10Fe/QES, 20Fe/QES and 30Fe/QES materials, respectively. The smallest bandgap of the 30Fe/QES material is possibly due to the highest purity of CaFe 2 O 4 (without impure CaO and Ca(OH) 2 ). Nevertheless, the 30Fe/QES sample gave an E g value that was quite high compared to that of the single phase CaFe 2 O 4 materials reported by previous studies with the values of 1.8-1.9 eV, corresponding to the absorption edge of 688-590 nm. [52][53][54] The small amount of CaCO 3 in the 30Fe/QES sample may contribute to the relatively high E g .
The inuences of % Fe loading on the morphology of the xFe/QES materials can be detected. The SEM image of QES eggshell particles in Fig. 4a showed various sizes of irregular granules with some pores on the surface, while the calcination, 750°C, 6 h, of QES resulted in smaller sizes of the irregularshaped and plate-like particles (Fig. 4e). Hydrothermal treatments of Fe-loaded QES gave irregular shaped samples having  slightly irregular morphologies with rougher surface in comparison to that of QES, Fig. 4b-d. From Fig. 4f-h, the morphology of the xFe/QES materials (x = % Fe loading) and phases (discussed earlier) depend on the % Fe loadings. Small needle-shaped particles of the 20Fe/QES and 30Fe/QES materials were observed, with 20Fe/QES having smaller and more uniform particle size.

Photocatalytic efficiency and reusability
The xFe/QES samples were applied as photocatalysts in the removal of 2-cholophenol (2-CP) from water. The use of a visible radiation light source to stimulate 2-CP breakdown was unsuccessful, giving negligible 2-CP removal efficiencies. A possible explanation for the poor photocatalytic activity under visible light irradiation is the low absorption intensity in the visible light range (Fig. 3). The aforementioned UV-vis light source was then used to explore the feasibility of the eggshellderived photocatalysts for 2-CP degradation.
The removal of 2-CP from water was investigated under a basic condition (pH 12). No addition of base (such as NaOH) was required, as adding 30Fe/QES into 2-CP (aq) resulted in a change in pH from 6.5 to 12 due to a trace amount of the CaO phase in the 30Fe/QES sample, as suggested by XPS and XRD results. Utilizing the 30Fe/QES photocatalyst bypasses the pH adjustment step that was necessary to achieve effective degradation of 2-CP in a previous work. 35 In addition, from a previous investigation, 55 CaFe 2 O 4 tends to be an ineffective photocatalyst under acidic conditions. Fig. 5a and b illustrates the absorption spectra of the aqueous 2-CP treated with 30Fe/QES. The 2-CP characteristic peaks at 237 nm and 294 nm were observed, in excellent agreement with a previous report. 2,34 The stability of 2-CP aer treatment in the dark of the 30Fe/QES sample, in Fig. 5a, suggested that there was no 2-CP removal. Hence, the photocatalytic reactions resulted in the 2-CP removal, as conrmed in Fig. 5b. From Fig. 5c, it can be seen that 8% removal of 2-CP is due to sorption (from treatment under dark condition). The highest 2-CP removal efficiency of 86.1 ± 1.0% was achieved from the 30Fe/QES treatment of 25 ppm 2-CP (aq) aer 180 min UV-vis illumination.
Furthermore, the photocatalytic activity of biobased materials in the degradation of aqueous 2-CP was examined by total organic carbon (TOC) analyses. The TOC removal efficiencies aer irradiation for 180 min obtained from treatments of 2-CP (aq) using various catalysts are displayed in Fig. 5d. The highest  TOC removal efficiency of ca. 50% was achieved, upon 2-CP (aq) abatement, by using the 30Fe/QES photocatalyst. Thus, the results in Fig. 5c and d suggested a complete conversion of 2-CP to degradation products. However, the products are sufficiently stable and half of 2-CP was mineralized to CO 2 and H 2 O. It should be noted that the bio-resourced CaO (QES-750) was found to be an ineffective photocatalyst, providing a TOC removal efficiency that was lower than 20%. The semiconducting properties of QES-750 are in a good agreement with another study that applied CaO/Ca(OH) 2 as photocatalyst in the decomposition of organic pollutants. [55][56][57] The results shown in Fig. 5 suggested that the UV-vis absorption technique may be not suitable to monitor and identify intermediates in this reaction system. Nonetheless, the incomplete TOC removal from the 30Fe/QES treatments provides evidence of stable 2-CP degradation products in the treated 2-CP solutions. The results suggested that the 30Fe/QES photocatalyst, with a relatively low bandgap energy, may be responsible for the high 2-CP removal efficiency. Additionally, the minor CaCO 3 phase in the 30Fe/QES photoactive material may promote the effective separation of the photogenerated electrons and holes, similar to another research work that indicated the improved photocatalytic degradation efficiencies of aqueous organic dyes (rhodamine B and methyl orange) over CaCO 3 /ZnO. 58 Furthermore, the 30Fe/QES was subjected to subsequent 2-CP removal runs without purication/ regeneration processes. It was found that the 30Fe/QES catalyst can be effectively reused, giving 2-CP removal efficiencies of 70.5% ± 0.99 in the 3rd cycle. Then, the efficiency decreased in the 4th cycle to 61.0% ± 1.98, as seen in Fig. 6d. The lower removal efficiencies may be due to the catalyst mass loss during multiple transfers of the catalyst in centrifugation and decantation steps.
From the FT-IR results (Fig. 6b), unclear absorption peaks corresponding to the CO 3 2− group of CaCO 3 at 1413, 873 and 712 cm −1 , Fe-O (586 cm −1 ) and Ca-O (450 cm −1 ) were observed, compared to fresh 30Fe/QES and aer reuse for 1 cycle. 59 In addition, the presence of peaks in the range of 1400-1600 cm −1 was detected, corresponding to aromatic derivative species (degraded products). The obtained results may suggest that the surface covering 2-CP degradation products, and chlorine poisons 60 could cause a lessening of the content of catalytic active sites on 30Fe/QES to effectively degrade 2-CP. From Fig. 6c, there is no evidence of the decomposition (photocorrosion) of calcium ferrite upon irradiation under basic conditions. Nonetheless, ion rearrangement in calcium ferrite took place aer treatments with 2-CP (aq), resulting in the structural transformation from the orthorhombic CaFe 2 O 4 to cubic CaFe 2 O 4 phase. 61 The spent 30Fe/QES photocatalyst contains both polymorphs.   process. 37 The loss of the OH group from hydroxyhydroquinone led to the generation of hydroquinone or catechol (m/z of 110), and further degraded to phenol (m/z of 96). Thereaer, the oxidation of phenol led to the formation of maleic acid or fumaric acid (m/z = 119). Notably, at reaction times of 120 and 180 min, the formation of acetic acid (m/z = 60) was detected, resulting from the degradation of maleic acid or fumaric acid, and further possibly degraded to smaller molecules into CO 2 and H 2 O and HCl, as reported in previous studies. 37,62 Results indicated that the breakdown of 2-CP requires at least 120 minutes to produce a substance that is less hazardous than 2-CP. The possible photodegradation products of 2-CP identied in Fig. 7 are quite similar to those in previous research studies. 36,62 Nonetheless, the characteristic masses (m/z) of some intermediates were slightly different from their theoretical molecular weight (±5) probably because the compound has secondary characteristic masses or low concentration, and was converted rapidly to CO 2 within the long reaction time. 37 Probing of the reactive oxygen species and holes under photocatalytic systems ESR spectra can be indicative evidence of the photogenerated radical species in the treated 2-CP (aq). The characteristic ESR signals corresponding to the DMPO/cOH adduct were previously reported elsewhere. [38][39][40] As shown in Fig. 8a, no ESR signals corresponding to the presence of the DMPO/cOH adduct were detected in systems related to the QES-750 or 30Fe/QES samples. This is possibly due to the alkaline characteristic of the treated 2-CP solutions, which is in good agreement with previous works that reported lower concentrations of the DMPO/cOH species in basic media. [65][66][67] On the other hand, to evaluate the O 2 c − radical formation (as shown in Fig. 8b), six peaks were observed in 2-CP (aq) treated with QES-750 and 30Fe/QES under UV-vis light irradiation for 60 min. However, the presence of such peaks does not match with the ESR prole of the O 2 c − radical samples. [37][38][39] The ESR signals with hyperne coupling constants (g), a N = 13.9, a Hb = 8.6 and a Hg = 1.6 agreed well with previous studies, indicating the formation of DMPO/cOCH 3 as the methanol molecules reacted with the photogenerated holes, giving the cOCH 3 species (CH 3 OH + h + / cOCH 3 + H + ). [38][39][40] Consequently, the photogenerated holes can be detected by ESR in the form of the DMPO/cOCH 3 species. Methoxide are preferred on the basic catalyst surface. The absence of a typical DMPO/cO 2 − prole (e − + O 2 / O 2 c − ) could be possibly due to the weak signal and/or overlapping position with the ESR peak corresponding to DMPO/cOCH 3 . Fig. 8c reports the values of the ESR peak areas corresponding to the density of the photogenerated hole in the treated 2-CP (aq) as a function of treatment times. From the results, the concentrations of the photogenerated holes in the treated 2-CP in decreasing order were obtained from the 30Fe/QES, 20Fe/QES, and 10Fe/QES treatments. A very low content of holes was generated in the QES750 treatments. Thus, Fe signicantly improved the stability of the holes species, as well as boost the formation of holes in the photodegradation of 2-CP.

Determination of the degradation products
Next, scavenger testing, another complementary analysis, was conducted to explore the inuences of possible reactive species (holes, O 2 c − and OHc radicals) on the 2-CP photocatalytic degradation. Comparative photocatalytic 2-CP degradation efficiencies with or without the addition of specic scavengers were measured aer each solution was treated under UV-vis irradiation for 60 min. As shown in Fig. 8d, the signicantly decreased 2-CP degradation efficiencies were obtained as ammonium oxalate (AO) was added into the system, giving only 26.0% compared with the control system (no scavenger, 53.3%). In addition, the degradation of 2-CP was slightly suppressed with the addition of benzoquinone for O 2 c − radical capture (48.4%). However, upon adding isopropyl alcohol (IPA) as the OHc scavenger, the degradation efficiencies were almost identical to that of the control system (56.8%). The scavenger testing results suggested that photogenerated holes played a major role. The O 2 c − radical had a minor inuence on 2-CP degradation, whereas the OHc radical should not be responsible for the effective 2-CP degradation under the condition studied. This conclusion agreed well with the ESR results, as previously discussed.
The overall photocatalytic degradation processes of 2-CP over CaFe 2 O 4 (30Fe/QES) are depicted in Fig. 9. Under light irradiation, the photogenerated electrons (e − ) were excited from the valence band (VB) to the conduction band (CB), leaving holes (h + ) at the VB of CaFe 2 O 4 . Based on the energy band structure of CaFe 2 O 4 , the hydroxy radicals could not be generated due the VB potential of CaFe 2 O 4 (+1.52 eV) being less positive than +2.38 eV (cOH/H 2 O, +2.38 eV vs. NHE). 63,68 Alternatively, the photogenerated holes in VB can oxidize the 2-CP molecules. In addition, the CB potential (−1.29 eV) of CaFe 2 O 4 was more negative than O 2 /O 2 c − (−0.33 V vs. NHE). The electrons in the CB can also reduce O 2 to O 2 c − , promoting the 2-CP degradation. From the energy band structure and scavenging study, it was noted that the photogenerated holes is a key radical active species for 2-CP degradation with the assistance of O 2 c − as a minor species. Table 1 lists previous research studies that used spinel ferrite-based photocatalysts for chlorophenol degradation. However, a direct comparison of the photocatalytic performances obtained from this work and other studies is not simple, as all experiments were conducted using different treatment conditions (concentrations and structures of chlorophenols, light source, treatment times and catalyst loading). Table 1 gives the best efficiency obtained from each research group. Firstly, the reusable ferrite-based catalysts (reuse without the requirement of washing and heating steps) for chlorophenol degradation are calcium ferrite (produced in this work) and the ZnFe 2 O 4 nanotube. 69 Li et al. reported that under visible light irradiation, the ZnFe 2 O 4 nanotube arrays derived from a sol-gel method provide a complete degradation of 4-chlorophenol (4-CP, 10 ppm) aer 360 min treatments. 69 The high photocatalytic performance of the ZnFe 2 O 4 nanotube arrays was attributed to their narrow band gap (1.85 eV) and efficient channel for the photo-generated electron-hole pair over a well-oriented nanotube structure. However, because the amount of the ZnFe 2 O 4 nanotube arrays catalyst was not clearly given, comparing the catalyst loading with this work is difficult. Despite being effective and reusable, the amount of 30Fe/QES required in the 2-CP degradation reactions was greater than previous works ( Table  1). The low catalyst loadings (0.3-1 g L −1 ) were applicable to give the chlorophenol degradation efficiency of 70% and above for ferrite based-composites (Chitosan/CoFe 2 O 4 , 35 CuFe 2 O 4 /TiO 2 , 70 and Cu 0.5 Mn 0.5 Fe 2 O 4 /TiO 2 70 ). The effective separation of electron-hole separation under light irradiation and higher surface area (high density of catalytic active sites) resulted in high chlorophenol photodegradation efficiencies using ferrite-based nanocomposites. 70 On the other hand, ZnFe 2 O 4 36 and CuFe 2 O 4 70 were ineffective in 4-CP degradation, and higher catalyst loading may be required to further improve the 4-CP degradation efficiency.
In comparison to prior ndings, the materials in previous studies required longer treatment time (240-360 min) and the photocatalyst syntheses required expensive chemical raw materials. 35,69,70 The advantages of using eggshell waste can be emphasized, as the Ca-rich waste derived CaFe 2 O 4 materials showed photocatalytic activity that was comparable to that of other spinel-based systems, in addition to reusability without the requirement of surface regeneration (e.g., washing, heat treatment and reactivation).

Conclusions
Calcium ferrite (CaFe 2 O 4 , E g = 2.81 eV) can be obtained, without CaO and Ca(OH) 2 impurity phases detected, by using waste eggshell as a natural source. The green CaFe 2 O 4 is applicable as a reusable photocatalyst in the oxidation of 2-chlorophenol (2-CP) under UV-vis light irradiation, achieving an 86.1% 2-CP removal efficiency. Photogenerated holes played the most important role in the radical pathway of 2-CP oxidation, compared with superoxide and hydroxyl radicals. Hydroxyl radicals were not detected in the reaction systems due to the band structure of calcium ferrite produced in this work and the alkaline conditions for 2-CP treatments. As eggshell waste is abundant and presumably renewable, manufacturing the ferrite catalyst on a larger scale should be feasible. From this work, the performance of eggshell-derived calcium ferrite should be further improved to lower the required catalyst loadings. Further research into potentially low-cost calcium ferrite-based composites may be carried out in order to achieve highperformance photocatalysts for various chemicaltransformation applications. The development of such composites could have signicant implications for environmental sustainability.

Conflicts of interest
The authors declare no conicts of interest.